Discrimination of thermodynamic models applied to supercritical-fluid extraction

被引:4
作者
Cassel, E [1 ]
deOliveira, JV [1 ]
机构
[1] UNIV FED SANTA CATARINA,DEPT CHEM ENGN,BR-88010970 FLORIANOPOLIS,SC,BRAZIL
关键词
model discrimination; supercritical-fluid extraction; high-pressure phase equilibria; parameter estimation; screening;
D O I
10.1016/S0896-8446(96)90038-8
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 [物理化学]; 081704 [应用化学];
摘要
Experimental planning associated with model discrimination is a technique aimed to optimize experimental procedures causing a cost reduction. Surprisingly, this technique has not been used extensively in phase-equilibrium experiments. Although this rationalization may not be so effective in vapor-liquid equilibrium at low pressures, the same is not true for systems at high pressures. This is the case when considering supercritical-fluid extraction (SCFE) where molecular asymmetry and the proximity to the critical point make modeling of such systems a challenging task. As it has been pointed out in the literature, the success of SCFE relies on the ability to predict and correlate the corresponding thermodynamic behavior. The objective of this work is to show that sequential model discrimination may be used as a rational method for obtaining experimental data, even when a simplified methodology is applied. Literature data on SCFE of two carbon dioxide containing systems were used along with current thermodynamic models. The results show that when model discrimination is applied, less experimental information is required as compared to conventional model selection, without any loss of fitting quality.
引用
收藏
页码:6 / 11
页数:6
相关论文
共 12 条
[1]
A NEW MIXING RULE MODIFIED CONVENTIONAL MIXING RULE [J].
ADACHI, Y ;
SUGIE, H .
FLUID PHASE EQUILIBRIA, 1986, 28 (02) :103-118
[2]
EVALUATION OF PARAMETERS FOR NON-LINEAR THERMODYNAMIC MODELS [J].
ANDERSON, TF ;
ABRAMS, DS ;
GRENS, EA .
AICHE JOURNAL, 1978, 24 (01) :20-29
[3]
Casselton L. A., 1994, MYCOTA, P307
[4]
FERRARIS GB, 1983, CHEM ENG SCI, V38, P225
[5]
MODELING THE VAPOR-LIQUID-EQUILIBRIA OF 1,1,1-TRICHLOROETHANE + CARBON-DIOXIDE AND TOLUENE + CARBON-DIOXIDE AT 308-K, 323-K, AND 353-K [J].
FINK, SD ;
HERSHEY, HC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (02) :295-306
[6]
VAPOR LIQUID EQUILIBRIA FOR BINARY-MIXTURES OF CARBON-DIOXIDE AND FATTY-ACID METHYL-ESTERS [J].
INOMATA, H ;
KONDO, T ;
HIROHAMA, S ;
ARAI, K ;
SUZUKI, Y ;
KONNO, M .
FLUID PHASE EQUILIBRIA, 1989, 46 (01) :41-52
[7]
GENERALIZED THERMODYNAMIC CORRELATION BASED ON 3-PARAMETER CORRESPONDING STATES [J].
LEE, BI ;
KESLER, MG .
AICHE JOURNAL, 1975, 21 (03) :510-527
[8]
MULTIPHASE HIGH-PRESSURE EQUILIBRIA IN TERNARY AQUEOUS SYSTEMS [J].
PANAGIOTOPOULOS, AZ ;
REID, RC .
FLUID PHASE EQUILIBRIA, 1986, 29 :525-534
[9]
Reid R.C., 1987, PROPERTIES GASES LIQ
[10]
DEVELOPMENT OF A NEW CUBIC EQUATION OF STATE FOR PHASE-EQUILIBRIUM CALCULATIONS [J].
SCHWARTZENTRUBER, J ;
RENON, H ;
WATANASIRI, S .
FLUID PHASE EQUILIBRIA, 1989, 52 :127-134